CN105642204A - Biomass hydrolysis device - Google Patents
Biomass hydrolysis device Download PDFInfo
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- CN105642204A CN105642204A CN201610103899.9A CN201610103899A CN105642204A CN 105642204 A CN105642204 A CN 105642204A CN 201610103899 A CN201610103899 A CN 201610103899A CN 105642204 A CN105642204 A CN 105642204A
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- biomass
- condensing tower
- hydrolysis kettle
- steam
- air inlet
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J15/00—Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; Apparatus specially adapted therefor
- B01J15/005—Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
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- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a biomass hydrolysis device and belongs to the field of chemical industrial technical equipment for biomass. The biomass hydrolysis device comprises a hydrolysis kettle and a closed residue discharge chamber, wherein a residue discharge port is formed in the bottom of the hydrolysis kettle and connected with the residue discharge chamber through a residue discharge pipe, a condensing tower is arranged in the residue discharge chamber, a nozzle is arranged at the upper part of the condensing tower, a steam inlet is arranged at the middle-lower part, a water outlet is arranged on one side of the bottom, a liquid gathering pipe located above the steam inlet is also arranged in the condensing tower, the upper part of the liquid gathering pipe is larger than that of the lower part, the nozzle and the lower part of the water outlet are connected with a circulating pool through pipelines, and a circulating pump is also arranged on the pipeline connected with the nozzle. The residue discharge chamber is set into a closed space, after the reaction in the hydrolysis kettle is finished, residual steam containing acid gas and waste residues are discharged into the residue discharge chamber, the residual steam enters the condensing tower via the steam inlet to be condensed into droplets to fall off and enter the circulating pool, acid gas is condensed for recovery, and the environment is protected.
Description
Technical field
The invention belongs to the chemical industry technical equipment field of biomass, be specifically related to a kind of biomass by hydrolyzation device.
Background technology
Levulic acid (LevulinicAcid, LA), has another name called 4-oxy pentanoic acid, LA or LA, its outward appearance is white plates or acicular crystal, it is inflammable, low toxicity, have hygroscopicity, does not release carbon dioxide, distill and decompose hardly under normal pressure during heating. Owing to levulic acid molecular structure containing the polyfunctional groups such as carbonyl, carboxyl, methyl and methylene, it is made both to have had the character of carboxylic acid, there is again the character of ketone, there is good chemical reactivity, can be esterified, replace, condensation and neutralization reaction etc., the products such as resin, medicine, pesticide, spice, solvent, coating, ink, rubber, plastic additive, lube oil additive and surfactant can be produced by levulic acid.
Levulic acid can obtain after generating monosaccharide further dehydration and piptonychia acid from cellulose hydrolysis, and cellulose is widely present in the biomass resource of nature, and therefore, how utilizing biomass resource to change into levulic acid becomes study hotspot. At present, studying more technique is be beneficial to biomass to add pyrohydrolysis in acid condition, and then prepared levulic acid, the method technique is simple, production cost is low, and its deficiency is in that, containing a certain amount of steam in waste residue after biomass by hydrolyzation, containing the sour gas such as byproduct formic acid, acetic acid in steam, if being expelled directly out, then the waste gas in waste residue can to environment, accordingly, it would be desirable to the steam discharged during to hydrolysis kettle deslagging reclaims.
Summary of the invention
Present invention aim at providing a kind of biomass by hydrolyzation device.
Based on object above, the present invention takes techniques below scheme:
A kind of biomass by hydrolyzation device, including hydrolysis kettle and airtight deslagging chamber, it is provided with slag-drip opening bottom described hydrolysis kettle, slag-drip opening is connected with deslagging chamber by scum pipe, condensing tower it is provided with in deslagging chamber, condensing tower top is provided with shower nozzle, middle and lower part is provided with air inlet, bottom side is provided with outlet, the mortar tube being positioned at above air inlet it is additionally provided with in described condensing tower, the upper diameter of mortar tube is more than lower diameter, described shower nozzle is connected with circulating water pool respectively through pipeline with outlet bottom, connects and is additionally provided with circulating pump on the pipeline of shower nozzle.
Being additionally provided with filtering ponds between described outlet and circulating water pool, filtering ponds are positioned at the outside on circulating water pool top, are provided with water inlet between circulating water pool and filtering ponds, it is ensured that the cleaning of the recirculated water in circulating water pool.
The entrance point place of described scum pipe is provided with in the circuit of electrical ball valve, electrical ball valve and circulating pump and is equipped with time-delay relay, when starting deslagging, controls electrical ball valve delayed startup; During closedown, control circulating pump time-delay closing, it is ensured that the steam in waste residue does not externally discharge.
Described hydrolysis kettle upper portion side wall is provided with catalyst inlet, and described catalyst inlet is connected to the feed liquor core pipe being positioned within hydrolysis kettle, and feed liquor core pipe is evenly distributed with liquid outlet, and the internal diameter sectional area of feed liquor core pipe is more than the area sum of liquid outlet. When being beneficial in hydrolysis reaction to hydrolysis kettle filling catalyst, catalyst uniformly sprays to the biomass in hydrolysis kettle under a certain pressure.
The uniform cylinder of steam it is additionally provided with in described hydrolysis kettle, the uniform cylinder of described steam is upper and lower bottomless, and its longitudinal section is inverted trapezoidal structure, and the uniform cylinder of described steam is evenly distributed with venthole, be beneficial to after hydrolysis kettle passes into steam, steam can in hydrolysis kettle uniformly through.
Being symmetrically arranged with two condensing towers in described deslagging chamber, condensing tower, near the port of export position of scum pipe, is beneficial to separating of steam and slag, reduces noise during deslagging simultaneously.
Described air inlet is made up of air inlet equally distributed on condensing tower sidewall.
Compared with prior art, the method have the advantages that
1) present invention arranges condensing tower by deslagging chamber being arranged in an airtight space and deslagging chamber; after having reacted in hydrolysis kettle; residual water vapor and waste residue containing sour gas enter deslagging chamber simultaneously; residual water vapor is condensed into drop through air inlet entrance condensing tower and falls; enter circulating water pool; sour gas carries out condensation reclaim, protect environment.
2) it is provided above mortar tube by the air inlet at condensing tower, can prevent condensed liquid from flowing out from air inlet along tower wall.
3) in hydrolysis kettle, it is provided with feed liquor core pipe, can carry out after partial hydrolysis completes, directly adding catalyst when not blood pressure lowering is lowered the temperature, improve hydrolysis efficiency in biomass.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Fig. 2 is condensing tower structural representation in Fig. 1.
Fig. 3 is the top view of Tu1Zhong deslagging chamber.
Detailed description of the invention
A kind of biomass by hydrolyzation device, such as Fig. 1, shown in Fig. 2 and Fig. 3, including hydrolysis kettle 1 and airtight deslagging chamber 2, described hydrolysis kettle 1 top is provided with charging aperture 14, two side, top is respectively equipped with catalyst inlet 15 and escape pipe 16, lower sides is provided with air inlet pipe 17, bottom is provided with slag-drip opening 3, catalyst inlet 15 is connected to the feed liquor core pipe 20 being positioned within hydrolysis kettle 1, feed liquor core pipe 20 is in inverted l-shaped structure, the vertical section lower end of feed liquor core pipe 20 is positioned at hydrolysis kettle 1 bottom, the vertical section of feed liquor core pipe 20 is evenly distributed with the liquid outlet that bore dia is 2mm, feed liquor core bore sectional area is the twice of liquid outlet area sum, the uniform cylinder 18 of steam that longitudinal section is inverted trapezoidal structure it is additionally provided with in hydrolysis kettle 1, on the uniform cylinder 18 of steam, under bottomless, its longitudinal section is inverted trapezoidal structure, the uniform cylinder 18 of described steam is evenly distributed with the venthole that bore dia is 8mm, the uniform cylinder 18 of steam is positioned at above air inlet pipe 17 near the position of air inlet pipe 17, slag-drip opening 3 is connected with deslagging chamber 2 by scum pipe 4, the entrance point place of scum pipe 4 is provided with electrical ball valve 13, two condensing towers 5 it are arranged with in deslagging chamber 2, condensing tower 5 is near the port of export position of scum pipe 4, condensing tower 5 top is positioned at outside deslagging chamber 2, condensing tower 5 top is provided with shower nozzle 6, middle and lower part is provided with air inlet 7, bottom side is provided with outlet 8, air inlet 7 is made up of equally distributed air inlet on condensing tower 5 sidewall, the mortar tube 9 being positioned at above air inlet 7 it is additionally provided with in described condensing tower 5, the upper diameter of mortar tube 9 is more than lower diameter, described shower nozzle 6 is connected with circulating water pool 10 by pipeline with outlet 8 bottom, the filtering ponds 12 built with stone it are additionally provided with between outlet 8 and circulating water pool 10, filtering ponds 12 are positioned at the outside on circulating water pool 10 top, water inlet 19 it is provided with between circulating water pool 10 and filtering ponds 12, water inlet 19 is positioned at the lower wall of filtering ponds 12, connect and the pipeline of shower nozzle 6 is additionally provided with circulating pump 11, the circuit of electrical ball valve 13 and circulating pump 11 is equipped with time-delay relay.
Work process: air inlet pipe 17 is connected to the low-pressure low-temperature steam steam of 0.6��1.0MPa (170��180 DEG C) pipeline and the high-temperature high-pressure steam steam of 2.0��2.5MPa (210��230 DEG C) pipeline, by biomass and catalyst (diluted mineral acid and FeCl3) mixing, pass into low-pressure vapor, in biomass, hemicellulose occurs once to be hydrolyzed, discharge the gas phase being once hydrolyzed simultaneously, when in biomass hydrolysis of hemicellulose complete after, switching pass into high-temperature high-pressure steam, in biomass cellulose invention secondary hydrolysis, the gas phase of discharge secondary hydrolysis simultaneously, until secondary hydrolysis terminates. when in hydrolysis kettle 1, pressure is down to 0.70MPa, electrical ball valve 13 is quickly opened (before deslagging, circulating pump 11 starts, deslagging again after recirculated water is normal, electrical ball valve 13 and circulating pump 11 can start simultaneously, it is respectively provided with time-delay relay, electrical ball valve 13 delayed startup), residual water vapor and waste residue enter deslagging chamber 2 under certain pressure effect simultaneously, residual water vapor enters condensing tower 5 from air inlet 7, the aqueous phase being atomized in uphill process in tower is condensed into drop and falls after filtering (filtration residue) and enter circulating water pool 10, what sour gas was only absorbed by the water simultaneously enters circulating water pool 10, recirculated water enters condensing tower 5 after circulating pump 11 is suppressed. after having worked, first close electrical ball valve 13, circulating pump 11 time-delay closing, it is to avoid steam enters in air.
Claims (7)
1. a biomass by hydrolyzation device, it is characterized in that, including hydrolysis kettle and airtight deslagging chamber, it is provided with slag-drip opening bottom described hydrolysis kettle, slag-drip opening is connected with deslagging chamber by scum pipe, condensing tower it is provided with in deslagging chamber, condensing tower top is provided with shower nozzle, middle and lower part is provided with air inlet, bottom side is provided with outlet, the mortar tube being positioned at above air inlet it is additionally provided with in described condensing tower, the upper diameter of mortar tube is more than lower diameter, described shower nozzle is connected with circulating water pool respectively through pipeline with outlet bottom, connects and is additionally provided with circulating pump on the pipeline of shower nozzle.
2. biomass by hydrolyzation device according to claim 1, it is characterised in that being additionally provided with filtering ponds between described outlet and circulating water pool, filtering ponds are positioned at the outside on circulating water pool top, are provided with water inlet between circulating water pool and filtering ponds.
3. biomass by hydrolyzation device according to claim 2, it is characterised in that the entrance point place of described scum pipe is provided with in the circuit of electrical ball valve, electrical ball valve and circulating pump and is equipped with time-delay relay.
4. biomass by hydrolyzation device according to claim 3, it is characterized in that, described hydrolysis kettle upper portion side wall is provided with catalyst inlet, described catalyst inlet is connected to the feed liquor core pipe being positioned within hydrolysis kettle, being evenly distributed with liquid outlet on feed liquor core pipe, the internal diameter sectional area of feed liquor core pipe is more than the area sum of liquid outlet.
5. biomass by hydrolyzation device according to claim 4, it is characterised in that being additionally provided with the uniform cylinder of steam in described hydrolysis kettle, the uniform cylinder of described steam is upper and lower bottomless, and its longitudinal section is inverted trapezoidal structure, the uniform cylinder of described steam is evenly distributed with venthole.
6. biomass by hydrolyzation device according to claim 5, it is characterised in that be symmetrically arranged with two condensing towers in described deslagging chamber, condensing tower is near the port of export position of scum pipe.
7. according to the arbitrary described biomass by hydrolyzation device of claim 1-6, it is characterised in that described air inlet is made up of air inlet equally distributed on condensing tower sidewall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610103899.9A CN105642204B (en) | 2016-02-26 | 2016-02-26 | A kind of biomass by hydrolyzation device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610103899.9A CN105642204B (en) | 2016-02-26 | 2016-02-26 | A kind of biomass by hydrolyzation device |
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| CN105642204A true CN105642204A (en) | 2016-06-08 |
| CN105642204B CN105642204B (en) | 2016-10-26 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201610103899.9A Expired - Fee Related CN105642204B (en) | 2016-02-26 | 2016-02-26 | A kind of biomass by hydrolyzation device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107235940A (en) * | 2017-06-29 | 2017-10-10 | 河南省科学院能源研究所有限公司 | A kind of method of vapor phase acid catalyzing cooperation ethyl acetate extraction production furfural |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1989010362A1 (en) * | 1988-04-26 | 1989-11-02 | Biofine Incorporated | Lignocellulose degradation |
| CA2223600A1 (en) * | 1995-06-07 | 1996-12-19 | Biofine Incorporated | Production of levulinic acid from carbohydrate-containing materials |
| US5859263A (en) * | 1996-05-22 | 1999-01-12 | Board Of Regents University Of Nebraska Lincoln | Method and apparatus for production of levulinic acid via reactive extrusion |
| CN201864677U (en) * | 2010-11-09 | 2011-06-15 | 河南省科学院能源研究所有限公司 | Device for coproduction of levulinate and furfural by biomass fractional hydrolysis |
| CN102219766A (en) * | 2011-04-01 | 2011-10-19 | 山东万盛环保科技发展有限公司 | Automatic acidless continuous furfural hydrolysis system |
| CN102414158A (en) * | 2009-03-11 | 2012-04-11 | 百帆科技有限责任公司 | Production of formic acid |
-
2016
- 2016-02-26 CN CN201610103899.9A patent/CN105642204B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1989010362A1 (en) * | 1988-04-26 | 1989-11-02 | Biofine Incorporated | Lignocellulose degradation |
| CA2223600A1 (en) * | 1995-06-07 | 1996-12-19 | Biofine Incorporated | Production of levulinic acid from carbohydrate-containing materials |
| US5859263A (en) * | 1996-05-22 | 1999-01-12 | Board Of Regents University Of Nebraska Lincoln | Method and apparatus for production of levulinic acid via reactive extrusion |
| CN102414158A (en) * | 2009-03-11 | 2012-04-11 | 百帆科技有限责任公司 | Production of formic acid |
| CN201864677U (en) * | 2010-11-09 | 2011-06-15 | 河南省科学院能源研究所有限公司 | Device for coproduction of levulinate and furfural by biomass fractional hydrolysis |
| CN102219766A (en) * | 2011-04-01 | 2011-10-19 | 山东万盛环保科技发展有限公司 | Automatic acidless continuous furfural hydrolysis system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107235940A (en) * | 2017-06-29 | 2017-10-10 | 河南省科学院能源研究所有限公司 | A kind of method of vapor phase acid catalyzing cooperation ethyl acetate extraction production furfural |
| CN107235940B (en) * | 2017-06-29 | 2020-07-31 | 河南省科学院能源研究所有限公司 | Method for producing furfural by gas-phase acid catalysis in cooperation with ethyl acetate extraction |
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| CN105642204B (en) | 2016-10-26 |
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| CB03 | Change of inventor or designer information |
Inventor after: Lei Tingzhou Inventor after: Li Zaifeng Inventor after: Lin Lu Inventor after: Xu Haiyan Inventor after: Yang Yantao Inventor after: Ren Suxia Inventor after: He Xiaofeng Inventor after: Yang Shuhua Inventor after: Zhu Jinling Inventor before: Li Zaifeng Inventor before: Zhu Jinling Inventor before: Lei Tingzhou Inventor before: Lin Lu Inventor before: Li Shunqing Inventor before: Xu Haiyan Inventor before: Yang Yantao Inventor before: Ren Suxia Inventor before: He Xiaofeng Inventor before: Yang Shuhua |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161026 Termination date: 20210226 |
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| CF01 | Termination of patent right due to non-payment of annual fee |